US11486034B2ActiveUtilityA1

Method of preparing ITO ceramic target with controllable grain size

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Assignee: UNIV ZHENGZHOUPriority: Mar 6, 2020Filed: May 13, 2020Granted: Nov 1, 2022
Est. expiryMar 6, 2040(~13.7 yrs left)· nominal 20-yr term from priority
C04B 35/636C23C 14/3414C04B 35/63416C04B 2235/786C04B 35/63424C04B 2235/3293C04B 35/6261C04B 35/64C04B 2235/6562C04B 2235/6567C04B 2235/5454C04B 2235/77C23C 14/35C04B 2235/6565C04B 35/634C04B 2235/608C04B 35/638C04B 2235/604C04B 2111/00224C04B 2235/3286C04B 35/457C23C 14/086C04B 2235/5445C04B 35/6263C04B 35/63444C04B 35/63468
49
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Claims

Abstract

A method of preparing an ITO ceramic target includes that: In2O3 powder with mass fraction of 90˜97 and SnO2 powder with mass fraction of 10˜3 are ball-milled and mixed with deionized water, diluent, binder and polymer material by a sand mill to obtain an ITO ceramic slurry with a solid content between 70˜80% and a viscosity between 120˜300 mpa·s, with an average particle size D50 of the mixed powder controlled at 100˜300 nm; the ITO ceramic slurry is shaped by a pressure grouting to obtain an ITO ceramic green body with a relative density of 58˜62%; the ITO ceramic green body is put into a degreasing and sintering integrated furnace, and under a degreasing temperature of 700˜800° C., the ITO ceramic target is degreased in an atmospheric oxygen atmosphere for the time set to 12˜36 hours; the temperature increases from the degreasing temperature to the first sintering temperature of 1,600˜1,650° C.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
       1. A method of preparing an ITO ceramic target with a controllable grain size, comprising:
 ball-milling and mixing In 2 O 3  powder with mass fraction of 90˜97 and SnO 2  powder with mass fraction of 10˜3 with deionized water, diluent, binder and polymer material by a sand mill to obtain an ITO ceramic slurry with a solid content between 70˜80% and a viscosity between 120˜300 mPa·s, with an average particle size D50 of the mixed powder in the ITO ceramic slurry is controlled at 200˜300 nm; 
 shaping the ITO ceramic slurry by a pressure grouting to obtain an ITO ceramic green body with a relative density of 58˜62%; 
 the ITO ceramic green body undergoing an integrated degreasing and sintering treatment to obtain the ITO ceramic target; wherein the integrated degreasing and sintering treatment includes: 
 putting the ITO green body into a degreasing and sintering integrated furnace; 
 heating the degreasing and sintering integrated furnace to a degreasing temperature of 700˜800° C., degreasing the ITO ceramic green body in an atmospheric oxygen atmosphere for a degreasing time set to 12 to 36 hours; 
 increasing the degreasing and sintering integrated furnace from the degreasing temperature to a first sintering temperature of 1,600˜1,650° C.; and 
 after increasing to the first sintering temperature, keeping the temperature at the first sintering temperature for 0˜60 min, then start to reduce the degreasing and sintering integrated furnace from the first sintering temperature to a second sintering temperature of 1,500˜1,540° C., and sintering the ITO target at the second sintering temperature in the atmospheric oxygen atmosphere, with temperature kept for 12 to 36 hours, to finally obtain the ITO ceramic target. 
 
     
     
       2. The method according to  claim 1 , wherein the mass fractions of In 2 O 3  powder and SnO 2  powder are 90 and 10. 
     
     
       3. The method according to  claim 1 , wherein the mass fractions of In 2 O 3  powder and SnO 2  powder are 95 and 5. 
     
     
       4. The method according to  claim 1 , wherein the mass fractions of In 2 O 3  powder and SnO 2  powder are 93 and 7. 
     
     
       5. The method according to  claim 1 , wherein a primary particle size distribution range of the In 2 O 3  powder is 80˜200 nm, and a primary particle size distribution range of the SnO 2  powder is 80˜200 nm. 
     
     
       6. The method according to  claim 1 , wherein the diluent includes polyacrylic or polycarboxylic acid diluent, the binder includes gum arabic, polyvinyl alcohol or acrylic resin, and the polymer material includes polyacrylamide. 
     
     
       7. The method according to  claim 1 , wherein said ball-milling and mixing is performed under vacuum depressurized conditions, the negative pressure not greater than 9 Pa. 
     
     
       8. The method according to  claim 1 , wherein a heating rate from a room temperature to the degreasing temperature is set to 1˜3° C./min. 
     
     
       9. The method according to  claim 1 , wherein a heating rate from the degreasing temperature to the first sintering temperature is set to 2˜5° C./min. 
     
     
       10. The method according to  claim 1 , wherein a cooling rate from the first sintering temperature to the second sintering temperature is set to 8˜16° C./min.

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